US4713155A - Method for preparation of phosphatide concentrates from vegetable oils - Google Patents

Method for preparation of phosphatide concentrates from vegetable oils Download PDF

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US4713155A
US4713155A US06/884,038 US88403886A US4713155A US 4713155 A US4713155 A US 4713155A US 88403886 A US88403886 A US 88403886A US 4713155 A US4713155 A US 4713155A
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sediment
electromagnetic field
oil
vegetable oil
treated
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US06/884,038
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Norair S. Arutjunian
Elena P. Kornena
Robert V. Kazarian
Natalya A. Ponomareva
Grigory V. Redko
Lidia T. Sakhno
Irina S. Zhidkova
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KRASNODARSKY POLITEKHINICHESKY INSTITUT USSR KRASNODAR ULITSA KRASNAYA 135
Krasnodarsky Politekhnichesky Institut
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Krasnodarsky Politekhnichesky Institut
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Priority to BE0/216894A priority Critical patent/BE905071A/en
Priority to GB8616764A priority patent/GB2192396B/en
Application filed by Krasnodarsky Politekhnichesky Institut filed Critical Krasnodarsky Politekhnichesky Institut
Priority to US06/884,038 priority patent/US4713155A/en
Priority to FR868610213A priority patent/FR2601382B1/en
Priority to DE19863624205 priority patent/DE3624205A1/en
Assigned to KRASNODARSKY POLITEKHINICHESKY INSTITUT, USSR, KRASNODAR, ULITSA KRASNAYA, 135 reassignment KRASNODARSKY POLITEKHINICHESKY INSTITUT, USSR, KRASNODAR, ULITSA KRASNAYA, 135 ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: ARUTJUNIAN, NORAIR S., KAZARIAN, ROBERT V., KORNENA, ELENA P., PONOMAREVA, NATALYA A., REDKO, GRIGORY V., SAKHNO, LIDIA T., ZHIDKOVA, IRINA S.
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    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00—Refining fats or fatty oils
    • C11B3/006—Refining fats or fatty oils by extraction
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J7/00—Phosphatide compositions for foodstuffs, e.g. lecithin

Definitions

  • the present invention relates to oil-and-fat branch of the food industry and more particularly it relates to the methods for preparation of phosphatide concentrates (lecithin) from vegetable oils.
  • Phosphatide concentrates are a valuable product extensively utilized in confectionery, baking, fat-and-oil and other branches of food industry.
  • the process of drying at 60°-90° C. fails to ensure maximum removal of moisture from phosphatide concentrate and, consequently, does not produce phosphatide concentrate with a low moisture content.
  • Moisture in phosphatide concentrate raises the acid number of oil separated from phosphatide concentrate and the colur of said concentrate, i.e. it impairs the quality of phosphatide concentrates.
  • the drying temperature of phospholipid sediment should be raised to 100° C. which also affects detrimentally the quality of phosphatide concentrates due to the formation of undesirable products, melanophospholipids, which increase the colour index of phosphatide concentrate, and due to an increase in the acid number of the oil separated from phosphatide concentrate.
  • An object of the present invention is to provide a method of preparation of phosphatide concentrate from vegetable oils which, without increasing the phospholipid sediment drying temperature, would produce phocphatide concentrates with a minimum moisture content, minimum acid number of the oil separated from phosphatide concentrate, and a minimum colour index of phosphatide concentrate.
  • the invention consists in that a method is proposed for preparation of phosphatide concentrates from vegetable oils comprising the treatment of crude vegetable oil with water or aqueous solution of electrolyte, separation of the phospholipid sediment from hydrated vegetable oil and drying said sediment in which, according to the invention, the sediment of phospholipides is treated before drying in electromagnetic field of 40 000-240 000 A/m strength at 50°-65° C.
  • the sediment of phospholipids may be treated either in a constant or variable electromagnetic field or in the field rotating at a speed of 500-3000 rpm.
  • the disclosed method for preparation of phosphatide concentrates from vegetable oils provides for:
  • the sediment of phospholipides is treated before drying at 50°-65° C. in an electromagnetic field of 40 000-240 000 A/m.
  • the disclosed method for preparation of phosphatide concentrates from vegetable oils is accomplished as follows.
  • Crude vegetable oil e.g. sunflower or soya oil
  • a hydrating agent e.g. water or aqueous solution of electrolyte, for example 0.3% aqueous solution of sodium chloride, or 0.1% aqueous solution of citric acid.
  • the amount of hydrating agent should be 1-3% of the mass of crude vegetable oil.
  • the sediment of phospholipides is separated from the hydrated vegetable oil by settling or centrifuging.
  • the separated sediment of phospholipids is treated at 50°-65° C. in electromagnetic field of 40 000-240 000 A/m and dried at 50°-70° C.
  • the sediment is treated in a constant or variable electromagnetic field or in the field rotating at a speed of 500-3 000 rpm.
  • the quality of phosphatide concentrates is assessed by the following indices: moisture content, colour index, acid number of the oil separated from phosphatide concentrate.
  • Crude sunflower oil, acid number 2.48 KOH and phospholipid content 0.58%, is treated at 20° C. with water in the amount of 2% of the mass of oil.
  • the sediment of phospholipids is separated from the hydrated vegetable oil by settling.
  • the separated sediment of phospholipids is treated at 50° C. in a constant electromagnetic field of 40 000 A/m and dried at 70° C.
  • Crude sunflower oil, acid number 2.48 mg KOH, phospholipid content 0.58%, is treated at 50° C. with 0.3% aqueous solution of sodium chloride taken in the amount of 1.5% of the mass of oil.
  • the sediment of phospholipides is separated from the hydrated vegetable oil by centrifuging, treated at 65° C. in a constant electromagnetic field, intensity 240 000 A/m, and dried at 65° C.
  • Crude sunflower oil, acid number 3.08 mg KOH, phospholipid content 0.65%, is treated at 70° C. with water in the amount of 1.0% of the mass of oil.
  • the sediment of phospholipids is separated from hydrated vegetable oil by settling, then treated at 60° C. in a constant electromagnetic field, intensity 160 000 A/m, and dried at 60° C.
  • Crude soya oil, acid number 1.92 mg KOH, phospholipid content 2.15%, is treated at 20° C. with 0.1% aqueous solution of citric acid in the amount of 1.5% of the mass of oil.
  • the sediment of phospholipids is separated from hydrated vegetable oil by centrifuging and treated at 65° C. in a variable electromagnetic field, intensity 40 000 A/m, then dried at 65° C.
  • Crude soya oil, acid number 1.92 mg KOH, phospholipid content 2.15%, is treated at 70° C. with 0.5% aqueous solution of sodium chloride in the amount of 2.5% of the mass of oil.
  • the sediment of phospholipids is separated from hydrated vegetable oil by settling and treated at 50° C. in a variable electromagnetic field, intensity 240 000 A/m, then dried at 50° C.
  • Crude soya oil, acid number 2.45 mg KOH, phospholipid content 1.58% is treated at 70° C. with 1% aqueous solution of citric acid in the amount of 1% of the mass of oil.
  • the sediment of phospholipids is separated from hydrated vegetable oil by centrifuging and treated at 55° C. in a variable electromagnetic field of 160 000 A/m at 65° C.
  • Crude sunflower oil, acid number 3.40 mg KOH, phospholipid content 0.85% is treated at 65° C. with water in the amount of 1.0% of the mass of oil.
  • the sediment of phospholipids is separated from hydrated vegetable oil by settling and treated at 50° C. in an electromagnetic field, strength 40 000 A/m, rotating at a speed of 3000 rpm, then dried at 60° C.
  • Crude soya oil, acid number 3.50 mg KOH, phospholipid content 2.75%, is treated at 60° C. with 0.1% aqueous solution of citric acid in the amount of 3.0% of the mass of oil.
  • the sediment of phospholipids is separated from hydrated vegetable oil by settling and treated at 65° C. in a rotating electromagnetic field, strength 240 000 A/m, rotating speed 500 rpm, then dried at 70° C.
  • Crude soya oil, acid number 2.50 mg KOH, phospholipid content 2.75%, is treated at 65° C. with 1% aqueous solution of sodium chloride in the amount of 2.5% of the mass of oil.
  • the sediment of phospholipids is separated from hydrated vegetable oil by centrifuging and treated at 50° C. in an electromagnetic field, strength 160 000 A/m, rotating at a speed of 1500 rpm, then dried at 65° C.
  • Crude sunflower oil, acid number 2.48 mg KOH, phospholipid content 0.58%, is treated at 70° C. with water taken in the amount of 2.0% of the mass of oil.
  • the sediment of phospholipids is separated from hydrated vegetable oil by settling and dried at 70° C.
  • Crude soya oil, acid number 1.92 mg KOH, phospholipid content 2.15% is treated at 50° C. with 0.5% aqueous solution of sodium chloride taken in the amount of 3.0% of the mass of oil.
  • the sediment of phospholipids is separated from hydrated vegetable oil by centrifuging and dried at 80° C.
  • the disclosed method permits lowering the drying temperature of phospholipide sediment (Examples 5 and 7) which, in turn, curtails the power consumption for the process of drying.

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Biochemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Fats And Perfumes (AREA)
  • Edible Oils And Fats (AREA)

Abstract

A method for preparation of phosphatide concentrates from vegetable oil comprising the treatment of crude vegetable oil with water or aqueous solution of electrolyte, separation of the sediment of phospholipids from hydrated vegetable oil, treating said sediment in an electromagnetic field, strength 40 000-240 000 A/m at 50 DEG -65 DEG C., and drying said sediment.

Description

FIELD OF APPLICATION
The present invention relates to oil-and-fat branch of the food industry and more particularly it relates to the methods for preparation of phosphatide concentrates (lecithin) from vegetable oils.
Phosphatide concentrates are a valuable product extensively utilized in confectionery, baking, fat-and-oil and other branches of food industry.
BACKGROUND OF THE INVENTION
Known in the prior art is a method for preparation of phosphatide concentrates comprising the treatment of crude vegetable oil with water of aqueous solution of electrolyte, separation of the sediment of phospholipides from hydrated vegetable oil by settling or centrifuging and drying said sediment at 60°-90° C. ("Production and Processing of Vegetable Oils and Fats. Handbook" Leningrad, VNIIZH, 1973, vol 2, pp 13-44; "Production Technology of Vegetable Oils" ed. V. M. Kopeysky and S. I. Danilchuk, Moscow, "Light and Food Industry" Publishers, 1982, pp 404-407).
However, this method is noted for the following disadvantages.
The process of drying at 60°-90° C. fails to ensure maximum removal of moisture from phosphatide concentrate and, consequently, does not produce phosphatide concentrate with a low moisture content. Moisture in phosphatide concentrate raises the acid number of oil separated from phosphatide concentrate and the colur of said concentrate, i.e. it impairs the quality of phosphatide concentrates. Besides, in order to remove the maximum amount of moisture from phosphatide concentrate the drying temperature of phospholipid sediment should be raised to 100° C. which also affects detrimentally the quality of phosphatide concentrates due to the formation of undesirable products, melanophospholipids, which increase the colour index of phosphatide concentrate, and due to an increase in the acid number of the oil separated from phosphatide concentrate.
BRIEF DESCRIPTION OF THE INVENTION
An object of the present invention is to provide a method of preparation of phosphatide concentrate from vegetable oils which, without increasing the phospholipid sediment drying temperature, would produce phocphatide concentrates with a minimum moisture content, minimum acid number of the oil separated from phosphatide concentrate, and a minimum colour index of phosphatide concentrate.
In accordance with this and other objects, the invention consists in that a method is proposed for preparation of phosphatide concentrates from vegetable oils comprising the treatment of crude vegetable oil with water or aqueous solution of electrolyte, separation of the phospholipid sediment from hydrated vegetable oil and drying said sediment in which, according to the invention, the sediment of phospholipides is treated before drying in electromagnetic field of 40 000-240 000 A/m strength at 50°-65° C.
The sediment of phospholipids may be treated either in a constant or variable electromagnetic field or in the field rotating at a speed of 500-3000 rpm.
The disclosed method for preparation of phosphatide concentrates from vegetable oils provides for:
improving the quality of phosphatide concentrates by reducing their moisture content, colour index and the acid number of the oil separated from phosphatide concentrate;
reduced the power cnsumption for drying the phospholipid sediment by drying said sediment at low temperatures.
As stated above, the sediment of phospholipides is treated before drying at 50°-65° C. in an electromagnetic field of 40 000-240 000 A/m.
The temperature of treating the sediment of phospholipids below 50° C. is not recommended, since these temperatures fail to yield positive effect.
Conversely, temperatures above 65° C. for treating the sediment of phospholipids are impracticable since they do not ensure any additional positive effect but involve extra power consumption.
The use of electromagnetic field with a strength below 40 000 A/m should be discouraged since these parameters deny the achievement of a positive effect.
The electromagnetic field with a strength above 240 000 A/m is impracticable for treating the sediment of phospholipides since the accomplishment of the method at these parameters fails to provide an additional positive effect and involves extra power consumption.
It is not recommended that the sediment of phospholipids be treated in the electromagnetic field rotating at speeds lower than 500 rpm since these parameters do not produce positive effect.
It is likewise inexpedient to treat the sediment of phospholipids in the electromagnetic field rotating at speeds higher than 3 000 rpm, since these parameters do not produce any additional positive effect but involve extra power consumption.
DETAILED DESCRIPTION OF THE INVENTION
The disclosed method for preparation of phosphatide concentrates from vegetable oils is accomplished as follows.
Crude vegetable oil, e.g. sunflower or soya oil, is treated at 20°-70° C. with a hydrating agent, e.g. water or aqueous solution of electrolyte, for example 0.3% aqueous solution of sodium chloride, or 0.1% aqueous solution of citric acid. The amount of hydrating agent should be 1-3% of the mass of crude vegetable oil. The sediment of phospholipides is separated from the hydrated vegetable oil by settling or centrifuging. The separated sediment of phospholipids is treated at 50°-65° C. in electromagnetic field of 40 000-240 000 A/m and dried at 50°-70° C. The sediment is treated in a constant or variable electromagnetic field or in the field rotating at a speed of 500-3 000 rpm.
The quality of phosphatide concentrates is assessed by the following indices: moisture content, colour index, acid number of the oil separated from phosphatide concentrate.
These indices are determined by the known methods described in "Practical Laboratory Training in Processing Fats" ed. N. S. Arutunian, Moscow, "Light and Food Industry" Publ. House, 1983, pp 32-36.
The present invention will become more fulls apparent from the following examples of its realization.
EXAMPLE 1
Crude sunflower oil, acid number 2.48 KOH and phospholipid content 0.58%, is treated at 20° C. with water in the amount of 2% of the mass of oil. The sediment of phospholipids is separated from the hydrated vegetable oil by settling. The separated sediment of phospholipids is treated at 50° C. in a constant electromagnetic field of 40 000 A/m and dried at 70° C.
EXAMPLE 2
Crude sunflower oil, acid number 2.48 mg KOH, phospholipid content 0.58%, is treated at 50° C. with 0.3% aqueous solution of sodium chloride taken in the amount of 1.5% of the mass of oil. The sediment of phospholipides is separated from the hydrated vegetable oil by centrifuging, treated at 65° C. in a constant electromagnetic field, intensity 240 000 A/m, and dried at 65° C.
EXAMPLE 3
Crude sunflower oil, acid number 3.08 mg KOH, phospholipid content 0.65%, is treated at 70° C. with water in the amount of 1.0% of the mass of oil. The sediment of phospholipids is separated from hydrated vegetable oil by settling, then treated at 60° C. in a constant electromagnetic field, intensity 160 000 A/m, and dried at 60° C.
EXAMPLE 4
Crude soya oil, acid number 1.92 mg KOH, phospholipid content 2.15%, is treated at 20° C. with 0.1% aqueous solution of citric acid in the amount of 1.5% of the mass of oil. The sediment of phospholipids is separated from hydrated vegetable oil by centrifuging and treated at 65° C. in a variable electromagnetic field, intensity 40 000 A/m, then dried at 65° C.
EXAMPLE 5
Crude soya oil, acid number 1.92 mg KOH, phospholipid content 2.15%, is treated at 70° C. with 0.5% aqueous solution of sodium chloride in the amount of 2.5% of the mass of oil. The sediment of phospholipids is separated from hydrated vegetable oil by settling and treated at 50° C. in a variable electromagnetic field, intensity 240 000 A/m, then dried at 50° C.
EXAMPLE 6
Crude soya oil, acid number 2.45 mg KOH, phospholipid content 1.58% is treated at 70° C. with 1% aqueous solution of citric acid in the amount of 1% of the mass of oil. The sediment of phospholipids is separated from hydrated vegetable oil by centrifuging and treated at 55° C. in a variable electromagnetic field of 160 000 A/m at 65° C.
EXAMPLE 7
Crude sunflower oil, acid number 3.40 mg KOH, phospholipid content 0.85% is treated at 65° C. with water in the amount of 1.0% of the mass of oil. The sediment of phospholipids is separated from hydrated vegetable oil by settling and treated at 50° C. in an electromagnetic field, strength 40 000 A/m, rotating at a speed of 3000 rpm, then dried at 60° C.
EXAMPLE 8
Crude soya oil, acid number 3.50 mg KOH, phospholipid content 2.75%, is treated at 60° C. with 0.1% aqueous solution of citric acid in the amount of 3.0% of the mass of oil. The sediment of phospholipids is separated from hydrated vegetable oil by settling and treated at 65° C. in a rotating electromagnetic field, strength 240 000 A/m, rotating speed 500 rpm, then dried at 70° C.
EXAMPLE 9
Crude soya oil, acid number 2.50 mg KOH, phospholipid content 2.75%, is treated at 65° C. with 1% aqueous solution of sodium chloride in the amount of 2.5% of the mass of oil. The sediment of phospholipids is separated from hydrated vegetable oil by centrifuging and treated at 50° C. in an electromagnetic field, strength 160 000 A/m, rotating at a speed of 1500 rpm, then dried at 65° C.
EXAMPLE 10 (comparative)
The method is accomplished under the conditions described in "Production and Processing of Vegetable Oils and Fats". Handbook., Leningrad, VNIIZH, 1973, pp 13-44.
Crude sunflower oil, acid number 2.48 mg KOH, phospholipid content 0.58%, is treated at 70° C. with water taken in the amount of 2.0% of the mass of oil. The sediment of phospholipids is separated from hydrated vegetable oil by settling and dried at 70° C.
EXAMPLE 11 (comparative)
The method is accomplished under the conditions described in "Production and Processing of Vegetable Oils and Fats". Handbook. Leningrad, VNIIZH 1973, pp 13-44.
Crude soya oil, acid number 1.92 mg KOH, phospholipid content 2.15% is treated at 50° C. with 0.5% aqueous solution of sodium chloride taken in the amount of 3.0% of the mass of oil. The sediment of phospholipids is separated from hydrated vegetable oil by centrifuging and dried at 80° C.
The data collected by accomplishing the method under the conditions stated in Examples 1 through 11 are summarized in the Table.
              TABLE                                                       
______________________________________                                    
Quality characteristics of phosphatide concentrate                        
         Colour    Moisture  Acid number, mg KOH                          
Example  index,    content   of oil separated from                        
No.      mg iodine %         phosphatide concentrate                      
1        2         3         4                                            
______________________________________                                    
1        12.0      0.58      10.57                                        
2        10.0      0.50      10.05                                        
3        11.0      0.45      11.59                                        
4        9.0       0.70      10.48                                        
5        8.0       0.60      9.85                                         
6        8.5       0.59      10.17                                        
7        11.5      0.65      12.00                                        
8        11.0      0.40      9.85                                         
9        10.5      0.45      10.52                                        
10       15.5      0.98      14.87                                        
(comparative)                                                             
11       15.5      0.98      15.49                                        
(comparative)                                                             
______________________________________
The results contained in the Table point to the fact that phosphatide concentrates produced in accordance with the disclosed method (Examples 1 through 9) feature a higher quality than do the phosphatide concentrates produced by the prior art method (Examples 10 and 11). Thus, the moisture content of phosphatide concentrates, the acid number of oil separated from phosphatide concentrate and the colour index of phosphatide concentrates produced in Examples 1 through 9 are lower than the respective indices in phosphatide concentrates produced in Examples 10 and 11.
Apart from that, the disclosed method permits lowering the drying temperature of phospholipide sediment (Examples 5 and 7) which, in turn, curtails the power consumption for the process of drying.

Claims (9)

What is claimed is:
1. A method for preparation of phosphatide concentrates from vegetable oils comprising treating crude vegetable oil with a hydrating agent selected from the group consisting of water and aqueous solutions of electrolytes, separating phospholipids from hydrated vegetable oil providing a phospholipid sediment, passing said sediment through an electromagnetic field with a strength of 40 000-24 000 Amperes/meter at 5°-65° C., and drying the treated phospholipid sediment.
2. The method according to claim 1 wherein the electromagnetic field is a constant electromagnetic field.
3. The method according to claim 1 wherein the electromagnetic field is a variable electromagnetic field.
4. The method according to claim 1 wherein the electromagnetic field is a rotating electromagnetic field rotating at a speed of 500-3 000 rpm.
5. The method according to claim 1 wherein the crude vegetable oil comprises sunflower oil.
6. The method according to claim 1 wherein the crude vegetable oil comprises soya oil.
7. The method according to claim 1 wherein the vegetable oil is treated with the hydrating agent at a temperature of 20°-70° C.
8. The method according to claim 1 wherein said hydrating agent comprises citric acid.
9. The method according to claim 1 wherein said hydrating agent comprises water in an amount of 1.0% by mass of vegetable oil.
US06/884,038 1986-07-10 1986-07-10 Method for preparation of phosphatide concentrates from vegetable oils Expired - Fee Related US4713155A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
BE0/216894A BE905071A (en) 1986-07-10 1986-07-08 PROCESS FOR OBTAINING PHOSPHATIDE CONCENTRATES FROM VEGETABLE OILS.
GB8616764A GB2192396B (en) 1986-07-10 1986-07-09 Method of preparing phosphatide concentrates from vegetable oils
US06/884,038 US4713155A (en) 1986-07-10 1986-07-10 Method for preparation of phosphatide concentrates from vegetable oils
FR868610213A FR2601382B1 (en) 1986-07-10 1986-07-11 PROCESS FOR OBTAINING PHOSPHATIDE CONCENTRATES FROM VEGETABLE OILS
DE19863624205 DE3624205A1 (en) 1986-07-10 1986-07-17 METHOD FOR PRODUCING PHOSPHATID CONCENTRATES FROM PLANT OILS

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DE (1) DE3624205A1 (en)
FR (1) FR2601382B1 (en)
GB (1) GB2192396B (en)

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US6172247B1 (en) 1998-11-20 2001-01-09 Ip Holdings, L.L.C. Methods for refining vegetable oils and byproducts thereof
US6423857B1 (en) 1998-11-20 2002-07-23 I.P. Holdings Methods for recovering fatty acids
US6426423B1 (en) 1998-11-20 2002-07-30 I.P. Holdings Methods for treating phosphatide-containing mixtures
US6441209B1 (en) 1998-11-20 2002-08-27 Ip Holdings, L.L.C. Method for treating organic acid-treated phosphatides
US20040030166A1 (en) * 2002-03-18 2004-02-12 Dick Copeland Methods for treating deodorizer distillate
US6750359B1 (en) 2001-09-04 2004-06-15 Ip Holdings, L.L.C. Methods for treating deodorizer distillate
US20040210070A1 (en) * 2001-07-23 2004-10-21 Marco Kruidenberg Method and apparatus for processing vegetable oils
US10851327B2 (en) 2018-06-11 2020-12-01 Poet Research, Inc. Methods of refining a grain oil composition feedstock, and related systems, compositions and uses
US11008531B2 (en) 2018-02-09 2021-05-18 Poet Research, Inc. Methods of refining a grain oil composition to make one or more grain oil products, and related systems
CN113214312A (en) * 2021-04-27 2021-08-06 内蒙古铂贝曼科技有限公司 Preparation method of active phospholipid lamellar liquid crystal
US11987832B2 (en) 2020-08-06 2024-05-21 Poet Research, Inc. Endogenous lipase for metal reduction in distillers corn oil

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RU2112783C1 (en) * 1996-12-24 1998-06-10 Учебно-научно-производственная фирма "Липиды" Line for hydrated oil and vegetable phospholipids production

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Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6172247B1 (en) 1998-11-20 2001-01-09 Ip Holdings, L.L.C. Methods for refining vegetable oils and byproducts thereof
US6172248B1 (en) 1998-11-20 2001-01-09 Ip Holdings, L.L.C. Methods for refining vegetable oils and byproducts thereof
US6423857B1 (en) 1998-11-20 2002-07-23 I.P. Holdings Methods for recovering fatty acids
US6426423B1 (en) 1998-11-20 2002-07-30 I.P. Holdings Methods for treating phosphatide-containing mixtures
US6441209B1 (en) 1998-11-20 2002-08-27 Ip Holdings, L.L.C. Method for treating organic acid-treated phosphatides
US20070129559A1 (en) * 2001-07-23 2007-06-07 Cargill, Incorporated Method and apparatus for processing vegetable oils
US20040210070A1 (en) * 2001-07-23 2004-10-21 Marco Kruidenberg Method and apparatus for processing vegetable oils
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GB2192396B (en) 1990-08-29
DE3624205A1 (en) 1988-01-28
FR2601382B1 (en) 1989-05-19
GB2192396A (en) 1988-01-13
FR2601382A1 (en) 1988-01-15
GB8616764D0 (en) 1986-08-13

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